EP3718724B1 - Method for recycling plastic nylon 6,6 from vacuum bags to obtain filaments for 3d printing processes - Google Patents
Method for recycling plastic nylon 6,6 from vacuum bags to obtain filaments for 3d printing processes Download PDFInfo
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- EP3718724B1 EP3718724B1 EP19382254.1A EP19382254A EP3718724B1 EP 3718724 B1 EP3718724 B1 EP 3718724B1 EP 19382254 A EP19382254 A EP 19382254A EP 3718724 B1 EP3718724 B1 EP 3718724B1
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- vacuum bags
- filaments
- printing processes
- extruder
- nylon
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/001—Combinations of extrusion moulding with other shaping operations
- B29C48/0022—Combinations of extrusion moulding with other shaping operations combined with cutting
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
- B29B17/04—Disintegrating plastics, e.g. by milling
- B29B17/0412—Disintegrating plastics, e.g. by milling to large particles, e.g. beads, granules, flakes, slices
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
- B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
- B29B7/40—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft
- B29B7/42—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft with screw or helix
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/58—Component parts, details or accessories; Auxiliary operations
- B29B7/66—Recycling the material
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/58—Component parts, details or accessories; Auxiliary operations
- B29B7/72—Measuring, controlling or regulating
- B29B7/726—Measuring properties of mixture, e.g. temperature or density
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/80—Component parts, details or accessories; Auxiliary operations
- B29B7/88—Adding charges, i.e. additives
- B29B7/885—Adding charges, i.e. additives with means for treating, e.g. milling, the charges
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B9/00—Making granules
- B29B9/12—Making granules characterised by structure or composition
- B29B9/14—Making granules characterised by structure or composition fibre-reinforced
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
- B29C48/05—Filamentary, e.g. strands
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/275—Recovery or reuse of energy or materials
- B29C48/277—Recovery or reuse of energy or materials of materials
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/92—Measuring, controlling or regulating
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C64/00—Additive manufacturing, i.e. manufacturing of three-dimensional [3D] objects by additive deposition, additive agglomeration or additive layering, e.g. by 3D printing, stereolithography or selective laser sintering
- B29C64/30—Auxiliary operations or equipment
- B29C64/357—Recycling
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B33—ADDITIVE MANUFACTURING TECHNOLOGY
- B33Y—ADDITIVE MANUFACTURING, i.e. MANUFACTURING OF THREE-DIMENSIONAL [3D] OBJECTS BY ADDITIVE DEPOSITION, ADDITIVE AGGLOMERATION OR ADDITIVE LAYERING, e.g. BY 3D PRINTING, STEREOLITHOGRAPHY OR SELECTIVE LASER SINTERING
- B33Y40/00—Auxiliary operations or equipment, e.g. for material handling
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B33—ADDITIVE MANUFACTURING TECHNOLOGY
- B33Y—ADDITIVE MANUFACTURING, i.e. MANUFACTURING OF THREE-DIMENSIONAL [3D] OBJECTS BY ADDITIVE DEPOSITION, ADDITIVE AGGLOMERATION OR ADDITIVE LAYERING, e.g. BY 3D PRINTING, STEREOLITHOGRAPHY OR SELECTIVE LASER SINTERING
- B33Y70/00—Materials specially adapted for additive manufacturing
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
- B29B2017/001—Pretreating the materials before recovery
- B29B2017/0021—Dividing in large parts
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
- B29B17/04—Disintegrating plastics, e.g. by milling
- B29B2017/042—Mixing disintegrated particles or powders with other materials, e.g. with virgin materials
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
- B29B17/04—Disintegrating plastics, e.g. by milling
- B29B2017/0424—Specific disintegrating techniques; devices therefor
- B29B2017/0468—Crushing, i.e. disintegrating into small particles
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
- B29B17/04—Disintegrating plastics, e.g. by milling
- B29B2017/0424—Specific disintegrating techniques; devices therefor
- B29B2017/0496—Pyrolysing the materials
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B9/00—Making granules
- B29B9/02—Making granules by dividing preformed material
- B29B9/06—Making granules by dividing preformed material in the form of filamentary material, e.g. combined with extrusion
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/92695—Viscosity; Melt flow index [MFI]; Molecular weight
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/92704—Temperature
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/9279—Errors or malfunctioning, e.g. for quality control
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C64/00—Additive manufacturing, i.e. manufacturing of three-dimensional [3D] objects by additive deposition, additive agglomeration or additive layering, e.g. by 3D printing, stereolithography or selective laser sintering
- B29C64/10—Processes of additive manufacturing
- B29C64/106—Processes of additive manufacturing using only liquids or viscous materials, e.g. depositing a continuous bead of viscous material
- B29C64/118—Processes of additive manufacturing using only liquids or viscous materials, e.g. depositing a continuous bead of viscous material using filamentary material being melted, e.g. fused deposition modelling [FDM]
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2077/00—Use of PA, i.e. polyamides, e.g. polyesteramides or derivatives thereof, as moulding material
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
- B29K2105/06—Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts
- B29K2105/12—Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts of short lengths, e.g. chopped filaments, staple fibres or bristles
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B29L2031/712—Containers; Packaging elements or accessories, Packages
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J11/00—Recovery or working-up of waste materials
- C08J11/04—Recovery or working-up of waste materials of polymers
- C08J11/06—Recovery or working-up of waste materials of polymers without chemical reactions
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
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- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Definitions
- the invention refers to methods for recycling plastic Nylon 6,6 from vacuum bags to obtain filaments for 3D printing of plastics, for instance by using Fused Filament Fabrication (FFF) printers and/or Selective Laser Sintering (SLS) printers.
- FFF Fused Filament Fabrication
- SLS Selective Laser Sintering
- 3D printed aeronautical flying or non-flying parts can be produced with recycled filaments or powder.
- non-flying parts tools or other manufacturing elements can be included.
- EP 3012078 A1 discloses a process that uses a starting material formed by recycled post-consumer and industrial "scrap" thermoplastics based on polyester and polyamide, and obtains a supply suitable for 3D printing/additive manufacturing/rapid prototyping with "Fused Deposition Model” (FDM), "Fused Filament Fabrication” (FFF) from these recycled thermoplastics.
- Said supply can have the form of a solid filament suitable to be used by said "3D” printers, or it can form a pulverulent material to be used in printers such as those with SLS technology.
- the method includes a series of first stages that consist of: a) Selecting the starting material, which was originally produced by one of the processes of transformation; b) said starting material is duly cleaned; c) once it is cleaned, the material is dried at temperatures greater than 100 oC but less than 240 oC; d) the material obtained thereof is driven into an extruder machine where it is subject to temperatures that will vary between 200 °C and 350 °C from the head to the dosing zone to be pelletized; e) the addition of additives to the material may occur in the feed zone in order to grant distinctive physicochemical properties to the end product, such as colour, hardness, erosion, strength f) from the material resulting from the previous stage either a plastic filament is created and is placed in a spool, or a pulverulent material is created.
- the supply obtained from the previous stages is subject to an additional heat treatment by varying the process temperature between 100 oC and 240°C, during a processing time varying between 1 minute and 24 hours.
- Nylon 6,6 is used without being combined and with short-fibre reinforcement for parts with no structural requirements in aircraft manufactured by classical methods, for example machining a round bar.
- it is used in the aeronautics industry for the design of prototypes and models as well as for the fabrication of drill templates.
- 3D printing also known as Additive Manufacturing
- additive Manufacturing is a technology with high advantages for application in aeronautical or other fields, which is now being widely developed and explored to get the full potential of it.
- plastics and reinforced plastics 3D printing are making their way in the market and showing also high potential for different applications (e.g. low loaded parts).
- the invention relates to a method in accordance with claim 1.
- the object of the invention is to provide methods for recycling plastic Nylon 6,6 from vacuum bags (for example, those used in aircraft part production) to obtain filaments for 3D printing processes, such that the scrap materials obtained in the production of composite parts can be reduced.
- the invention provides a method for recycling plastic Nylon 6,6 from vacuum bags to obtain filaments for 3D printing processes, that comprises the following steps:
- the invention presents several advantages, related to the recycling of a material, which is supposed to be used just once, for an innovative application / use (3D printing):
- the invention refers to methods for recycling plastic Nylon 6,6 from vacuum bags 2 (for example, those used in aircraft part production) to obtain filaments 9 or powder for 3D printing processes, particularly for the production of aircraft parts.
- the filaments 9 are used for Fused Filament Fabrication (FFF) and the powder for Selective Laser Sintering (SLS).
- FFF Fused Filament Fabrication
- SLS Selective Laser Sintering
- Recycled filaments 9 may be obtained with or without reinforcement from production vacuum bags 2 and CFRP scraps.
- a quality control step is needed. This control should be performed periodically, including visual inspection to detect any change of colour, appearance, rigidity or flexibility that involves crystallinity degree modification, and/or concentration of resin residues, and thermal analysis, such as Thermogravimetry (TMA), to detect potential effect in different parameters, such as weight loss percentage.
- TMA Thermogravimetry
- a quality control may be performed periodically at the end of the recycling process to check out if the final product (filament) has the specified / needed properties for the application.
- the process of adding virgin material is not mandatory, but helps to improve the quality of the re-used material.
- a quality control of the smaller pieces 3 or the pellets is performed after the previous step.
- This quality control step comprises one or more of the following controls:
- the smaller pieces 3 or the pellets are introduced in an extruder 15 with a motor 8 for the purpose of producing the filaments 9.
- the smaller pieces 3 or the pellets go through a hopper 4 and they are melted in the central part of the extruder 15 (Barrel 5 and Screw 6) at a temperature above the melting temperature of Nylon 6,6 ( ⁇ 273 oC).
- cut virgin Nylon 6,6 can also be added (for example, in a 50:50 proportion, or in any other proportion) and melted together.
- the melt/molten mixture is expelled from the extruder 15 by the die 7, which shapes the melt/molten mixture in the planned filaments 9 (1.75-3 mm diameter) due to the drop of temperature.
- the length of this step depends on the number of used vacuum bags 2 that provide the small cut pieces 3 or the pellets and on the quantity of needed virgin Nylon 6,6 in case of mixing.
- the outdoor temperature or a cooler facilitates the cooling and the solidification right after the die 7. Furthermore, the filaments 9 can also be dyed later.
- virgin Nylon 6,6 could also be added together with the vacuum bags 2 (for example, in a 50:50 proportion, or in any other proportion) to the same grinder 1 and then melted together.
- filaments 9 can be reinforced adding different fibres such us carbon, glass or aramid fibres or other reinforcements such as CNTs, Graphene, carbon black, nanoparticles, etc.
- recycled fibres for example, Recycled Short Fibre: Recycled SF in figures 5A and 5B
- fibre reinforced plastics scrap obtained during aeronautical part production, through standard process of pyrolysis or solvolysis and applying also a grinding/cutting process to obtain cut fibre, that needs to be fed also to the extrusion process in combination with the plastic, Nylon 6,6, smaller pieces 3 or the pellets.
- the reinforcement can be obtained in a compounding step before the extrusion step, in which the smaller pieces 3 or the pellets and fibre reinforcements are introduced in a set of extruder and cutter for the compounding step to obtain reinforced smaller pieces or reinforced pellets to be used in the extrusion step.
- each coil 10 has to have around 270 meters of filament 9 rolled up on itself.
- Figure 4 shows a schematic representation of a winder 16 with an intermediate pulley 11, a pulley 12, a motor 13 and a tension bearing 14, and the winding process.
- a quality control step is needed. This control should be performed periodically, including: visual inspection to detect any change of colour, appearance, rigidity or flexibility that involves crystallinity degree modification, and/or concentration of resin residues, and thermal analysis, such as Thermogravimetry (TMA), to detect potential effect in different parameters, such as weight loss percentage.
- TMA Thermogravimetry
- a quality control may be performed periodically at the end of the recycling process to check out if the final product (powder) has the specified properties.
- vacuum bags 2 are brought into a grinder 1 that produces very little pieces (powder with particles of 0.1 mm diameter) by cutting them up.
- Used vacuum bags 2 could also be mixed (in a 50:50 proportion, or in any other proportion) with virgin Nylon 6,6 to improve the quality of the used material, providing as well powder particles with 0,1 mm diameter.
- recycled Nylon/virgin Nylon 6,6 can also be mixed in the desired proportion with small pieces of Carbon or Glass Fibres as well as any other reinforcements, recycled (obtained from CFRP scrap through pyrolysis or solvolysis and cutting/grinding process to obtain powder) or not-recycled.
- a quality control of the powder is performed after the grinding step.
- This quality control step comprises one or more of the following controls:
- the resulting powder is ready to be used in 3D SLS printers.
- the mixing could be performed at the same time inside the same grinder 1 or each material could be cut up in a different grinder and then the provided powders would be mixed (50:50).
- Additive manufacturing by means of FFF technology with recycled filaments 9 seems to be a good option for non-loaded applications with low rate production or where high NRC investments are required. Additive manufacturing technology appears as a better option versus other technologies (injection moulding%) for these applications.
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- Materials Engineering (AREA)
- Environmental & Geological Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Physics & Mathematics (AREA)
- Optics & Photonics (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Air Bags (AREA)
- Artificial Filaments (AREA)
Description
- The invention refers to methods for recycling
6,6 from vacuum bags to obtain filaments for 3D printing of plastics, for instance by using Fused Filament Fabrication (FFF) printers and/or Selective Laser Sintering (SLS) printers.plastic Nylon - 3D printed aeronautical flying or non-flying parts can be produced with recycled filaments or powder. As examples of non-flying parts, tools or other manufacturing elements can be included.
- Nowadays raw plastics which are base of the Fused Filament Fabrication (FFF) filaments or the powder for Selective Laser Sintering (SLS) processes are obtained from virgin materials. The same situation is observed for the fibre reinforcements: they are obtained from the classical manufacturing methods known for the raw fibres.
- Currently, there is not any process or procedure for the recycling of vacuum bags which are extensively used for curing processes of prepreg materials and/or vacuum based infusion processes such as LRI, VARTM, RFI, etc.
- Nevertheless, there are some methods and processes for the recycling of polyamides. As Nylon 6,6, the material that vacuum bags are made of, is part of the polyamides family, this opens the possibility of finding a second life for this material that is extensively used in the composites industry and can be re-used in other applications.
- So far, current methods for recycling polyamides carry out processes of depolymerisation and repolymerisation, as disclosed in the following patent documents:
-
US 8366977 B2 : Process of making recycled polyamide yarn. -
US 2004/0249001 A1 : Process for the solution recovery of nylon with high reactivity and articles made therefrom. -
US 6187917 B1 : Process for the purification of caprolactam obtained from the depolymerasation of polyamide-containing carpet. -
US 2004/0186190 A1 : Solvent-based recovery and recycle polyamide material. -
EP 3012078 A1 discloses a process that uses a starting material formed by recycled post-consumer and industrial "scrap" thermoplastics based on polyester and polyamide, and obtains a supply suitable for 3D printing/additive manufacturing/rapid prototyping with "Fused Deposition Model" (FDM), "Fused Filament Fabrication" (FFF) from these recycled thermoplastics. Said supply can have the form of a solid filament suitable to be used by said "3D" printers, or it can form a pulverulent material to be used in printers such as those with SLS technology. The method includes a series of first stages that consist of: a) Selecting the starting material, which was originally produced by one of the processes of transformation; b) said starting material is duly cleaned; c) once it is cleaned, the material is dried at temperatures greater than 100 ºC but less than 240 ºC; d) the material obtained thereof is driven into an extruder machine where it is subject to temperatures that will vary between 200 °C and 350 °C from the head to the dosing zone to be pelletized; e) the addition of additives to the material may occur in the feed zone in order to grant distinctive physicochemical properties to the end product, such as colour, hardness, erosion, strength f) from the material resulting from the previous stage either a plastic filament is created and is placed in a spool, or a pulverulent material is created. The supply obtained from the previous stages is subject to an additional heat treatment by varying the process temperature between 100 ºC and 240°C, during a processing time varying between 1 minute and 24 hours. - Regarding recycled reinforcement fibres, currently there are developed processes for obtaining fibres from carbon fibre reinforced processes like the pyrolysis or the solvolysis. These activities are acquiring more importance due to the interest of several industries, like the automotive one.
- However, so far these reinforcements are not used to reinforce Additive Manufacturing filaments, they are mostly used for non-highly loaded components manufactured by short fibre reinforcement moulding.
- Currently, Nylon 6,6 is used without being combined and with short-fibre reinforcement for parts with no structural requirements in aircraft manufactured by classical methods, for example machining a round bar. In addition, it is used in the aeronautics industry for the design of prototypes and models as well as for the fabrication of drill templates.
- Nowadays, one of the main issues associated to the increase of composite parts in aircrafts is the amount of material scrap / waste obtained in production plants, which highly affects part life cycle:
- Auxiliary materials / vacuum bags: during part curing processes (Autoclave or OoA), a large amount of vacuum bags are needed, which are thrown away once curing processes are performed.
- Composite / fibre reinforced plastics (FRP) scrap: in addition, tons of CFRP scrap are obtained during part production, which are nowadays mostly buried.
- In fact, this problem could be greater in the future with the expected environmental regulation changes, which may limit material waste. Therefore solutions are needed as soon as possible to reduce and/or recycle the material waste obtained in composite part production.
- On the other hand, 3D printing (also known as Additive Manufacturing) is a technology with high advantages for application in aeronautical or other fields, which is now being widely developed and explored to get the full potential of it. Particularly, plastics and reinforced plastics 3D printing are making their way in the market and showing also high potential for different applications (e.g. low loaded parts).
- The invention relates to a method in accordance with
claim 1. - Dependent claims refer to preferred embodiments of the invention.
- In particular, the object of the invention is to provide methods for recycling
6,6 from vacuum bags (for example, those used in aircraft part production) to obtain filaments for 3D printing processes, such that the scrap materials obtained in the production of composite parts can be reduced.plastic Nylon - The invention provides a method for recycling
6,6 from vacuum bags to obtain filaments for 3D printing processes, that comprises the following steps:plastic Nylon - providing used Nylon 6,6 vacuum bags,
- quality control step to check the status of the used vacuum bags,
- step to form smaller parts from the used vacuum bags:
- the vacuum bags are cut into films, the films are rolled up and then are introduced into a set of extruder and cutter to obtain pellets,
- quality control step to check the status of the pellets,
- extrusion step: the pellets are introduced into an extruder, where they are melted, and the molten mixture is cooled and expelled through the die of the extruder to produce the recycled filaments, and
- winding step: the recycled filaments that go out of the extruder are rolled up in coils.
- The invention presents several advantages, related to the recycling of a material, which is supposed to be used just once, for an innovative application / use (3D printing):
- Positive environmental impact / life Cycle assessment:
- ∘
6,6 of the vacuum bag allows the bag to be reused for a completely different and innovative target from the previous one.Recycling Nylon - ∘ Reinforcements from fibre reinforced plastics can be reused by introducing them in the product life cycle again instead of burying them.
- ∘ Make 3D printing processes more attractive from environmental point / life cycle assessment of view.
- ∘
- Positive economic / cost impact:
- ∘ Mitigate the costs of new plastics and reinforcements purchase, raw materials for the 3D printing processes / parts.
- ∘ Mitigate the costs both economical and of brand image of waste production and treatment.
- ∘ Potential sales of a recycled product to other industries (outside aerospace field).
- Other characteristics and advantages of the present invention will be clear from the following detailed description of several embodiments illustrative of its object in relation to the attached figures.
-
-
Figure 1A shows a schematic diagram of the method for recycling 6,6 from vacuum bags to obtain unreinforced filaments for 3D printing processes, in a first alternative, which does not fall within the scope of the claims.plastic Nylon -
Figure 1B shows a schematic diagram of the method for recycling 6,6 from vacuum bags to obtain unreinforced filaments for 3D printing processes of the invention, in a second alternative.plastic Nylon -
Figure 2 shows a schematic representation of a grinder machine offigure 1A . -
Figure 3 shows a schematic representation of an extruder offigure 1A . -
Figure 4 shows a schematic representation of a winder offigure 1A or1B and the winding process. -
Figure 5A shows a schematic diagram of the method for recycling 6,6 from vacuum bags to obtain reinforced filaments for 3D printing processes, in a first alternative, which does not fall within the scope of the claims.plastic Nylon -
Figure 5B shows a schematic diagram of the method for recycling 6,6 from vacuum bags to obtain reinforced filaments for 3D printing processes of the invention, in a second alternative.plastic Nylon -
Figure 6 shows a schematic diagram of the method for recycling 6,6 from vacuum bags to obtain powder for 3D printing processes, which does not fall within the scope of the claims.plastic Nylon - The invention refers to methods for recycling
6,6 from vacuum bags 2 (for example, those used in aircraft part production) to obtain filaments 9 or powder for 3D printing processes, particularly for the production of aircraft parts.plastic Nylon - The filaments 9 are used for Fused Filament Fabrication (FFF) and the powder for Selective Laser Sintering (SLS).
- Recycled filaments 9 may be obtained with or without reinforcement from
production vacuum bags 2 and CFRP scraps. - The process / steps to be followed to recycle vacuum bag 2 (
Nylon 6,6), including the 3D printing filament production, are described hereafter: - In order to control if
vacuum bags 2 have suffered any kind of problem, a quality control step is needed. This control should be performed periodically, including visual inspection to detect any change of colour, appearance, rigidity or flexibility that involves crystallinity degree modification, and/or concentration of resin residues, and thermal analysis, such as Thermogravimetry (TMA), to detect potential effect in different parameters, such as weight loss percentage. - Moreover, a quality control may be performed periodically at the end of the recycling process to check out if the final product (filament) has the specified / needed properties for the application.
- Once
vacuum bags 2 have been used for curing processes (Autoclave or OoA: Out-of-Autoclave), and after being analysed (if needed), they are picked up and they can: - a) (which does not fall under the scope of the present invention) Be brought into a
grinder 1 where they are cut up in smaller minute pieces 3 (for instance, 0,5x0,5cm) that lead to a quicker melting due to their larger superficial area. Different piece sizes can be considered depending on the overall areal weight of thevacuum bag 2 material.
This process is almost immediate, thus, as thevacuum bags 2 go into thegrinder 1, thesmall cut pieces 3 leave thegrinder 1 in a non-stop process. Hence, the length of this step depends on the number of usedvacuum bags 2 and in case of mixing, on the quantity of 6,6 which follows the same procedure, or:virgin Nylon - b) Be cut into films, then the films are rolled up and then are introduced into a set of extruder and cutter to obtain pellets.
- As indicated, the process of adding virgin material is not mandatory, but helps to improve the quality of the re-used material.
- A quality control of the
smaller pieces 3 or the pellets is performed after the previous step. This quality control step comprises one or more of the following controls: - thermal analysis, such as Differential Scanning Calorimetry (DSC), to detect changes in Glass Transition Temperature (Tg), melting temperature (Tm) or extent of crystallinity, and
- molecular weight analysis, such as Gel Permeation Chromatography (GPC).
- The
smaller pieces 3 or the pellets are introduced in anextruder 15 with amotor 8 for the purpose of producing the filaments 9. To do so, thesmaller pieces 3 or the pellets go through ahopper 4 and they are melted in the central part of the extruder 15 (Barrel 5 and Screw 6) at a temperature above the melting temperature ofNylon 6,6 (≈273 ºC). As indicated, cut 6,6 can also be added (for example, in a 50:50 proportion, or in any other proportion) and melted together. Finally, the melt/molten mixture is expelled from thevirgin Nylon extruder 15 by thedie 7, which shapes the melt/molten mixture in the planned filaments 9 (1.75-3 mm diameter) due to the drop of temperature. As for the first step, the length of this step depends on the number of usedvacuum bags 2 that provide thesmall cut pieces 3 or the pellets and on the quantity of needed 6,6 in case of mixing.virgin Nylon - The outdoor temperature or a cooler facilitates the cooling and the solidification right after the
die 7. Furthermore, the filaments 9 can also be dyed later. - In the first step,
6,6 could also be added together with the vacuum bags 2 (for example, in a 50:50 proportion, or in any other proportion) to thevirgin Nylon same grinder 1 and then melted together. - As mentioned, filaments 9 can be reinforced adding different fibres such us carbon, glass or aramid fibres or other reinforcements such as CNTs, Graphene, carbon black, nanoparticles, etc. Relevant for this proposal is the introduction of recycled fibres (for example, Recycled Short Fibre: Recycled SF in
figures 5A and5B ) coming from fibre reinforced plastics scrap obtained during aeronautical part production, through standard process of pyrolysis or solvolysis and applying also a grinding/cutting process to obtain cut fibre, that needs to be fed also to the extrusion process in combination with the plastic, 6,6,Nylon smaller pieces 3 or the pellets. - The reinforcement can be obtained in a compounding step before the extrusion step, in which the
smaller pieces 3 or the pellets and fibre reinforcements are introduced in a set of extruder and cutter for the compounding step to obtain reinforced smaller pieces or reinforced pellets to be used in the extrusion step. - Tests conducted adding different fibre percentages in weight were carried out satisfactory, 30% and 40% trials are prepared.
- As the
6,6 filaments 9 go out of therecycled Nylon extruder 15 reinforced or unreinforced, they are rolled up incoils 10 by using a winding process. In order to be placed in the 3D printing device, eachcoil 10 has to have around 270 meters of filament 9 rolled up on itself. -
Figure 4 shows a schematic representation of awinder 16 with anintermediate pulley 11, apulley 12, amotor 13 and a tension bearing 14, and the winding process. - The following steps describe the process used to recycle the
vacuum bag 2 material (Nylon 6,6) as 3D printing powder material: - In order to control if
vacuum bags 2 have suffered any kind of problem, a quality control step is needed. This control should be performed periodically, including: visual inspection to detect any change of colour, appearance, rigidity or flexibility that involves crystallinity degree modification, and/or concentration of resin residues, and thermal analysis, such as Thermogravimetry (TMA), to detect potential effect in different parameters, such as weight loss percentage. - Moreover, a quality control may be performed periodically at the end of the recycling process to check out if the final product (powder) has the specified properties.
- After curing processes and being analysed (if needed),
vacuum bags 2 are brought into agrinder 1 that produces very little pieces (powder with particles of 0.1 mm diameter) by cutting them up. -
Used vacuum bags 2 could also be mixed (in a 50:50 proportion, or in any other proportion) with 6,6 to improve the quality of the used material, providing as well powder particles with 0,1 mm diameter.virgin Nylon - Additionally, during this step recycled Nylon/
6,6 can also be mixed in the desired proportion with small pieces of Carbon or Glass Fibres as well as any other reinforcements, recycled (obtained from CFRP scrap through pyrolysis or solvolysis and cutting/grinding process to obtain powder) or not-recycled.virgin Nylon - A quality control of the powder is performed after the grinding step. This quality control step comprises one or more of the following controls:
- thermal analysis, such as Differential Scanning Calorimetry (DSC), to detect changes in Glass Transition Temperature (Tg), melting temperature (Tm) or extent of crystallinity, and
- molecular weight analysis, such as Gel Permeation Chromatography (GPC).
- The resulting powder is ready to be used in 3D SLS printers.
- The mixing could be performed at the same time inside the
same grinder 1 or each material could be cut up in a different grinder and then the provided powders would be mixed (50:50). - Additive manufacturing by means of FFF technology with recycled filaments 9 seems to be a good option for non-loaded applications with low rate production or where high NRC investments are required. Additive manufacturing technology appears as a better option versus other technologies (injection moulding...) for these applications.
Claims (9)
- Method for recycling plastic Nylon 6,6 from vacuum bags (2) to obtain filaments (9) for 3D printing processes, that comprises the following steps:- providing used Nylon 6,6 vacuum bags (2),- quality control step to check the status of the used vacuum bags (2),- step to form smaller parts from the used vacuum bags:- the vacuum bags (2) are cut into films, the films are rolled up and then are introduced into a set of extruder and cutter to obtain pellets,- quality control step to check the status of the pellets,- extrusion step: the pellets are introduced into an extruder (15), where they are melted, and the molten material is cooled and expelled through the die (7) of the extruder (15) to produce the recycled filaments (9), and- winding step: the recycled filaments (9) that go out of the extruder (15) are rolled up in coils (10).
- Method for recycling plastic Nylon 6,6 from vacuum bags (2) to obtain filaments (9) for 3D printing processes, according to claim 1, that additionally comprises a compounding step before the extrusion step, in which the pellets and fibre reinforcements are introduced in a set of extruder and cutter for the compounding step to obtain reinforced pellets to be used in the extrusion step.
- Method for recycling plastic Nylon 6,6 from vacuum bags (2) to obtain filaments (9) for 3D printing processes, according to claim 1, that additionally comprises the addition of fibre reinforcements in the extruder (15) to obtain reinforced filaments (9).
- Method for recycling plastic Nylon 6,6 from vacuum bags (2) to obtain filaments (9) for 3D printing processes, according to any of the previous claims, that additionally comprises the addition of an anti-hydrolysis additive into the set of extruder and cutter to avoid humidity absorption in the step to form smaller parts to obtain pellets.
- Method for recycling plastic Nylon 6,6 from vacuum bags (2) to obtain filaments (9) for 3D printing processes, according to claims 2 or 3, wherein the fibre reinforcements are virgin fibres.
- Method for recycling plastic Nylon 6,6 from vacuum bags (2) to obtain filaments (9) for 3D printing processes, according to claim 2, wherein the fibre reinforcements are recycled fibres obtained from fibre reinforced plastics scraps obtained during aircraft part production.
- Method for recycling plastic Nylon 6,6 from vacuum bags (2) to obtain filaments (9) for 3D printing processes, according to claim 6, wherein the recycled fibres are obtained through a process of pyrolysis or solvolysis followed by a grinding or cutting process to obtain cut fibre.
- Method for recycling plastic Nylon 6,6 from vacuum bags (2) to obtain filaments (9) for 3D printing processes, according to any of the previous claims, that additionally comprises the addition of virgin Nylon 6,6 in the step to form smaller parts from the used vacuum bags and/or in the extruder (15).
- Method for recycling plastic Nylon 6,6 from vacuum bags (2) to obtain filaments (9) for 3D printing processes, according to any of the previous claims, in which the quality control step to check the status of the used vacuum bags (2) comprises one or more of the following controls:- visual inspection to detect any change of colour, appearance, rigidity or flexibility that involves crystallinity degree modification and/or concentration of resin residues, and- thermal analysis, such as Thermogravimetry, to detect weight loss percentage,and the quality control step to check the status of the cut pieces (3) before the extrusion step comprises one or more of the following controls:- thermal analysis, such as Differential Scanning Calorimetry, to detect changes in Glass Transition Temperature, melting temperature or extent of crystallinity, and- molecular weight analysis, such as Gel Permeation Chromatography.
Priority Applications (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP19382254.1A EP3718724B1 (en) | 2019-04-05 | 2019-04-05 | Method for recycling plastic nylon 6,6 from vacuum bags to obtain filaments for 3d printing processes |
| ES19382254T ES2949328T3 (en) | 2019-04-05 | 2019-04-05 | Methods for recycling Nylon 6,6 plastic from vacuum bags to obtain filaments for 3D printing processes |
| CN202080027443.3A CN113692336A (en) | 2019-04-05 | 2020-04-06 | Method for recycling nylon 6,6 plastic from vacuum bags to obtain filaments or powder for 3D printing processes |
| PCT/ES2020/070229 WO2020201609A1 (en) | 2019-04-05 | 2020-04-06 | Methods for recycling nylon 6,6 plastic from vacuum bags to obtain filaments or powder for 3d printing processes |
| US17/601,249 US12594694B2 (en) | 2019-04-05 | 2020-04-06 | Methods for recycling plastic Nylon 6,6 from vacuum bags to obtain filaments or powder for 3D printing processes |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP19382254.1A EP3718724B1 (en) | 2019-04-05 | 2019-04-05 | Method for recycling plastic nylon 6,6 from vacuum bags to obtain filaments for 3d printing processes |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP3718724A1 EP3718724A1 (en) | 2020-10-07 |
| EP3718724B1 true EP3718724B1 (en) | 2023-05-31 |
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ID=66323798
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP19382254.1A Active EP3718724B1 (en) | 2019-04-05 | 2019-04-05 | Method for recycling plastic nylon 6,6 from vacuum bags to obtain filaments for 3d printing processes |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US12594694B2 (en) |
| EP (1) | EP3718724B1 (en) |
| CN (1) | CN113692336A (en) |
| ES (1) | ES2949328T3 (en) |
| WO (1) | WO2020201609A1 (en) |
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| US20210402650A1 (en) * | 2020-06-30 | 2021-12-30 | Fibrecycle Materials Corp. | Method of manufacturing feedstock from recycled-fibers |
| JP2023062429A (en) * | 2021-10-21 | 2023-05-08 | 株式会社日立製作所 | Manufacturing method, manufacturing support method and system |
| IT202200000095A1 (en) * | 2022-01-14 | 2023-07-14 | Pielleitalia S R L | Manufacturing process and material for additive manufacturing |
| KR102797154B1 (en) * | 2022-05-17 | 2025-04-22 | 울산과학기술원 | Products and Overmolding process of 3D printing with recycled composite materials |
| CN115044194B (en) * | 2022-07-10 | 2024-04-26 | 江苏中江材料技术研究院有限公司 | 3D printing of recycled materials from waste nylon fishing nets and preparation method thereof |
| CN115214140B (en) * | 2022-07-22 | 2023-06-23 | 贵州省冶金化工研究所 | High recovery rate application method of selective laser printing powder |
| CN115416251A (en) * | 2022-09-15 | 2022-12-02 | 海安县恒业制丝有限公司 | Extruder for preparing nylon 6 filament and filament preparation process thereof |
| CN115922968B (en) * | 2022-12-16 | 2023-11-14 | 无锡纯宇环保制品有限公司 | Waste recycling structure of environment-friendly clothing packaging bag production equipment |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5129813A (en) * | 1991-02-11 | 1992-07-14 | Shepherd G Maury | Embossed vacuum bag, methods for producing and using said bag |
| JP3566348B2 (en) * | 1994-09-20 | 2004-09-15 | アイン・エンジニアリング株式会社 | A method and an apparatus for collecting and granulating a waste resin molded product, and a method for manufacturing a wooden synthetic board using the collected resin material. |
| JP3303610B2 (en) * | 1995-07-12 | 2002-07-22 | カルソニックカンセイ株式会社 | Recycling method of glass fiber reinforced polyamide |
| US5990306A (en) | 1997-09-03 | 1999-11-23 | Alliedsignal Inc. | Process for the purification of caprolactam obtained from the depolymerization of polyamide-containing carpet |
| WO2001094457A2 (en) | 2000-06-08 | 2001-12-13 | Dupont Canada Inc. | Solvent-based recovery and recycle of polyamide material |
| JP2006505419A (en) * | 2002-04-12 | 2006-02-16 | エムビーエー ポリマーズ, インコーポレイテッド | Multistage separation of plastic |
| US20040053047A1 (en) * | 2002-09-17 | 2004-03-18 | Jackson Craig A. | Colorable filaments from polymer blend |
| US20040249001A1 (en) | 2003-06-06 | 2004-12-09 | Christian Leboeuf | Process for the solution recovery of nylon with high reactivity and articles made therefrom |
| IL195283A (en) | 2008-11-13 | 2013-01-31 | Nilit Ltd | Process for manufacturing polyamide yarns utilizing polyamide waste |
| FR2964108B1 (en) * | 2010-08-26 | 2013-10-04 | Rhodia Operations | RECYCLING OF INFLATABLE SAFETY CUSHIONS BASED ON POLYAMIDE |
| AR100196A1 (en) * | 2014-10-21 | 2016-09-21 | Enye Tech S A | METHOD FOR DEVELOPING AN INPUT FROM THE RECYCLING OF PLASTIC MATERIAL OF INDUSTRIAL WASTE AND POST CONSUMPTION, SUITABLE TO BE USED BY 3D PRINTERS |
| CN104672757B (en) * | 2015-03-02 | 2018-02-16 | 苏州容坤半导体科技有限公司 | A kind of axial percent thermal shrinkage is less than 0.5% 3D printing wire rod, process of preparing and manufacture device |
| TW201821535A (en) * | 2016-07-29 | 2018-06-16 | 巴斯夫歐洲公司 | Polyamide blends comprising a reinforcing agent for laser sinter powder |
| FR3056435B1 (en) * | 2016-09-26 | 2019-05-31 | Armor | METHOD OF PRODUCING DENSIFIED MATERIAL FROM COMPLEX FILM, PRODUCTION PLANT AND USE. |
| KR102050362B1 (en) * | 2017-05-22 | 2019-12-02 | 재단법인 한국탄소융합기술원 | Manufacturing Method for Polymer composite with carbon fiber for 3D printers |
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- 2020-04-06 WO PCT/ES2020/070229 patent/WO2020201609A1/en not_active Ceased
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Also Published As
| Publication number | Publication date |
|---|---|
| EP3718724A1 (en) | 2020-10-07 |
| US12594694B2 (en) | 2026-04-07 |
| US20220184857A1 (en) | 2022-06-16 |
| WO2020201609A1 (en) | 2020-10-08 |
| ES2949328T3 (en) | 2023-09-27 |
| CN113692336A (en) | 2021-11-23 |
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